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dc.contributor.authorGelves, German
dc.contributor.authorNiño, Lilibeth
dc.contributor.authorHernandez, S
dc.date.accessioned2021-11-27T16:42:09Z
dc.date.available2021-11-27T16:42:09Z
dc.date.issued2020-11-04
dc.identifier.urihttp://repositorio.ufps.edu.co/handle/ufps/1496
dc.description.abstractIn this paper, the effects of some empirical scale up criteria (Reynold´s number and Impeller power per bioreactor volume) on gas-liquid mass transfer and microbial growth rates are analyzed using computational fluid dynamics simulations in a stirred tank bioreactor. The effects of turbulence, fluid flow and bubbles dynamics were simulated by using a two equation turbulence model, a multiple reference frame and a population balance, respectively. The impeller power per bioreactor volume scale up criterion showed better microbial growth rates than Reynold´s number scale up criterion. However, high cellular damage due to turbulence in animal cell culturing are still challenges in large scale up bioreactor prototyping.eng
dc.format.extent6 páginasspa
dc.format.mimetypeapplication/pdfspa
dc.language.isoengspa
dc.publisherJournal of Physics: Conference Seriesspa
dc.relation.ispartofJournal of Physics: Conference Series ISSN: 1742-6596, 2020 vol:1655 fasc: N/A págs: 1 - 6, DOI:10.1088/1742-6596/1655/1/012109
dc.rightsContent from this work may be used under the terms of theCreative Commons Attribution 3.0 licence. Any further distribution of this work must maintain attribution to the author(s) and the title of the work, journal citation and DOI. Published under licence by IOP Publishing Ltdeng
dc.sourcehttps://iopscience.iop.org/article/10.1088/1742-6596/1655/1/012109spa
dc.titleSimulating of Microbial Growth Scale Up in a Stirred Tank Bioreactor for Aerobic Processes using Computational Fluid Dynamicseng
dc.typeArtículo de revistaspa
dcterms.referencesNiño L, Gelves R, Ali H, Solsvik J and Jakobsen H 2019 Applicability of a modified breakage and coalescence model based on the complete turbulence spectrum concept for CFD simulation of gas-liquid mass transfer in a stirred tank reactor Chemical Engineering Science 211 1spa
dcterms.referencesGelves R, Benavides A and Quintero J C F D 2013 prediction of hydrodynamic behavior in the scale-up of a stirred tank reactor for aerobic processes Ingeniare Revista Chilena de ingeniería 21 347spa
dcterms.referencesGelves G 2020 Simulating hydrodynamics in a Rushton turbine at different stirring velocities applied to non-Newtonian fluids Journal of Physics: Conference Series 1587 012012spa
dcterms.referencesRutherford K, Lee, Mahmoudi K and Yianneskis M 1996 Hydrodynamic characteristics of dual Rushton impeller stirred vessels American Intitute of Chemical Engineering 42 332spa
dcterms.referencesKerdouss F, Bannari A, Proulx P, Bannari R, Skrga M and Labrecque Y 2012 Two-phase mass transfer coefficient prediction in a stirred vessel with a CFD model Computers and Chemical Engineering 32 1943spa
dcterms.referencesLuo J, Issaand R and Gosman A 1994 Prediction of impeller induced flow in mixing vessels using multiple frames of reference Chemical Engineering Symposium Series. Institution of Chemical Engineers 136 549spa
dcterms.referencesMicale G, Brucato and A Grisafi F 1999 Prediction of flow fields in a dual-impeller stirred tank American Intitute of Chemical Engineering 45(3) 445spa
dcterms.referencesTabor A, Gosman G and Issa R 1996 Numerical simulation of the flow in a mixing vessel stirred by a Rushton Turbine American Intitute of Chemical Engineering Symposium Series 140 25spa
dcterms.referencesSolsvik J and Jakobsen H 2016 A review of the statistical turbulence theory required extending the population balance closure models to the entire spectrum of turbulence American Intitute of Chemical Engineering 62(5) 1795spa
dc.identifier.doi10.1088/1742-6596/1655/1/012109
dc.publisher.placeReino Unidospa
dc.relation.citationeditionVol. 1655, 012109 (2020)spa
dc.relation.citationendpage6spa
dc.relation.citationstartpage1spa
dc.relation.citationvolume1655spa
dc.relation.citesHernandez, S., Niño, L. y Gelves, G. (2020). Simulating of microbial growth scale up in a stirred tank bioreactor for aerobic processes using computational fluid dynamics. Journal of Physics: Conference Series, 1655, Artículo 012109. https://doi.org/10.1088/1742-6596/1655/1/012109
dc.relation.ispartofjournalJournal of Physics: Conference Seriesspa
dc.rights.accessrightsinfo:eu-repo/semantics/openAccessspa
dc.rights.creativecommonsAtribución 4.0 Internacional (CC BY 4.0)spa
dc.type.coarhttp://purl.org/coar/resource_type/c_6501spa
dc.type.contentTextspa
dc.type.driverinfo:eu-repo/semantics/articlespa
dc.type.redcolhttp://purl.org/redcol/resource_type/ARTspa
oaire.accessrightshttp://purl.org/coar/access_right/c_abf2spa
oaire.versionhttp://purl.org/coar/version/c_970fb48d4fbd8a85spa
dc.type.versioninfo:eu-repo/semantics/publishedVersionspa


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